Calcium removal optimisation

Patent metadata

Field	Value
Publication number	US-11242491-B2
Application number	US-201816624898-A
Country	US
Kind code	B2
Filing date	Jun 6, 2018
Priority date	Jun 19, 2017
Publication date	Feb 8, 2022
Grant date	Feb 8, 2022

Abstract

A process for optimising the removal of calcium from a hydrocarbon feedstock in a refinery desalting process, the refinery desalting process comprising the following steps: (a) mixing one or more wash water streams with one or more hydrocarbon feedstock streams; (b) at least partially separating the wash water from the hydrocarbons in a refinery desalter; and (c) removing the separated water and hydrocarbons from the refinery desalter as one or more desalted hydrocarbon streams and one or more effluent water streams; the process optimisation comprising: (i) providing at least one x-ray fluorescence analyser at at least one point in the refinery desalting process; (ii) measuring the concentration of calcium at the at least one point in the process using the at least one x-ray fluorescence analyser; and (iii) optionally adjusting at least one process condition of the refinery desalting process in response to the calcium concentration measurement in step (ii). An apparatus comprises a desalter; a line through which one or more hydrocarbon feedstock streams are passed to the desalter; optionally a line through which one or more wash water streams are passed to the desalter; and one or more x-ray fluorescence analysers configured so as to measure the concentration of calcium in water or hydrocarbons at one or more positions within the apparatus.

First claim

The invention claimed is:

1. A process for optimising the removal of calcium from a hydrocarbon feedstock in a refinery desalting process, wherein the refinery desalting process comprises the following steps:
(a) mixing one or more wash water streams with one or more hydrocarbon feedstock streams;
(b) at least partially separating the wash water from the hydrocarbons in a refinery desalter; and
(c) removing the separated water and hydrocarbons from the refinery desalter as one or more desalted hydrocarbon streams and one or more effluent water streams;
wherein the process optimisation comprises:
(i) providing at least one x-ray fluorescence analyser at at least one point in the refinery desalting process;
(ii) measuring the concentration of calcium at the at least one point in the process using the at least one x-ray fluorescence analyser; and
(iii) optionally adjusting at least one process condition of the refinery desalting process in response to the calcium concentration measurement in step (ii); and
wherein the process optimisation further comprises measuring at least one additional process parameter selected from the pH of the one or more wash water streams, the pH of the one or more effluent water streams, the pH of the mixture of the water and hydrocarbons, the iron concentration at at least one point in the process, the amine concentration at at least one point in the process, and any combination thereof.

2. A process according to claim 1 , wherein step (ii) comprises on-line measurement of the calcium concentration.

3. A process according to claim 1 , wherein the step b) of at least partially separating the wash water from the hydrocarbons in a refinery desalter comprises applying an electric field to the water and the hydrocarbons present in the refinery desalter.

4. A process according to claim 1 , wherein the hydrocarbon feedstock comprises sodium chloride, calcium chloride, magnesium chloride, or any combination thereof.

5. A process according to claim 1 , wherein the one or more wash water streams and one or more hydrocarbon feedstock streams are mixed prior to being introduced into the refinery desalter or in the refinery desalter.

6. A process according to claim 1 , wherein removing calcium from the hydrocarbons during the refinery desalting process comprises the step of adding an acid, a solids wetter, a reverse breaker, a calcium scale inhibitor or any combination thereof to the one or more wash water streams, the one or more hydrocarbon feedstock streams, the mixture of hydrocarbons and water, or any combination thereof.

7. A process according to claim 1 , wherein the calcium is present in the hydrocarbon feedstock stream in the form of a calcium salt.

8. A process according to claim 7 , wherein the calcium salt is dissolved in the one or more hydrocarbon feedstock streams, dissolved in water residual in the one or more hydrocarbon feedstock streams, suspended within the one or more hydrocarbon feedstock streams, suspended within water residual in the one or more hydrocarbon feedstock streams, or any combination thereof.

9. A process according to claim 1 , wherein the measurement of the at least one additional process parameter comprises on-line measurement.

10. A process according to claim 1 , wherein the removing calcium from the hydrocarbons during the refinery desalting process further comprises the step of adding at least one acid to the mixture of water and hydrocarbons, the one or more wash water streams, the one or more hydrocarbon feedstock streams, or any combination thereof; and wherein step (iii) of adjusting at least one process condition of the refinery desalting process in response to the calcium concentration measurement in step (ii) comprises adjusting the rate of addition of the acid.

11. A process according to claim 1 , wherein the removing calcium from the hydrocarbons during the refinery desalting process further comprises the step of adding a calcium scale inhibitor to the mixture of water and hydrocarbons, the one or more wash water streams, the one or more hydrocarbon feedstock streams, or any combination thereof; and wherein step (iii) of adjusting at least one process condition of the refinery desalting process in response to the calcium concentration measurement in step (ii) comprises adjusting the rate of introduction of the calcium scale inhibitor.

12. A process according to claim 11 , wherein the calcium scale inhibitor comprises phosphonobutane-1,2,4-tricarboxylic acid (PBTC), amino-trimethylene phosphonic acid (ATMP) 1-hydroxyethylidene-1,1-diphosphonic acid (HEDP), polyacrylic acid (PAA), a phosphinopolyacrylate,a polymaleic acid (PMA), a maleic acid terpolymer (MAT), a sulfonic acid copolymer, or any combination thereof.

13. A process according to claim 1 , wherein step (ii) of measuring the concentration of calcium at the at least one point in the process using the at least one X-ray fluorescence analyser comprises measuring the concentration of calcium in the one or more desalted hydrocarbon streams or the one or more hydrocarbon feedstock streams, or both.

14. A process according to claim 13 , wherein step (ii) of measuring the concentration of calcium at the at least one point in the process using the at least one X-ray fluorescence analyser comprises measuring the concentration of calcium in the one or more effluent water streams.

15. A process according to claim 13 , wherein the process further comprises measuring the pH of the wash water stream, the pH of the effluent water stream, or both.

16. A process according to claim 13 , wherein removing calcium from the hydrocarbons during the refinery desalting process further comprises the step of adding an acid, a solids wetter, a reverse breaker, a calcium scale inhibitor or any combination thereof to the one or more wash water streams, the one or more hydrocarbon feedstock streams, the mixture of water and hydrocarbons, or any combination thereof; and wherein the step (iii) of adjusting the at least one process condition of the refinery desalting process comprises adjusting the rate of introduction of the acid, the solids wetter, the reverse breaker, the calcium scale inhibitor or any combination thereof.

17. A process according to claim 1 , wherein step (ii) of measuring the concentration of calcium at the at least one point in the process using the at least one x-ray fluorescence analyser and/or the optional step of measuring at least one additional process parameter comprises both on-line measurements and laboratory measurements.

18. A process according to claim 1 , wherein step (iii) of optionally adjusting at least one process condition of the refinery desalting process in response to the calcium concentration measurement in step (ii) comprises adjusting any one or more of the following desalting process parameters: temperature within the refinery desalter; pressure within the refinery desalter; mix valve drop pressure; rate of introduction of the one or more hydrocarbon feedstock streams; rate of introduction of the one or more wash water streams; the strength of the electric field applied in the refinery desalter; the presence, absence, or amount of one or more additives in the wash water stream or hydrocarbon feedstock stream; the concentration of acid, solids wetter, or reverse breaker, or calcium scale inhibitor if used; or any combination thereof.

19. A process according to claim 1 , wherein step (iii) of optionally adjusting at least one process condition of the refinery desalting process in response to the calcium concentration m

Assignees

• Bp Corp North America Inc

Inventors

• English Jason
• Hackett Craig

Classifications

• G01N2223/076

  X-ray fluorescence · CPC title

• G01N23/223

  by irradiating the sample with X-rays or gamma-rays and by measuring X-ray fluorescence · CPC title

• C10G31/08 Primary

  by treating with water · CPC title

• C10G17/04

  Liquid-liquid treatment forming two immiscible phases · CPC title

• G01N33/241

  for hydrocarbon content · CPC title